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United States Patent |
5,733,425
|
Fang
,   et al.
|
March 31, 1998
|
Titanium alloy anode for electrolyzing manganese dioxide
Abstract
This invention relates to a titanium alloy anode for the electrolytic
production of manganese dioxide, wherein the alloy anode is made of
titanium as a base metal, and comprises at least three other metals
selected from the group consisting of manganese, chromium, iron, silicon,
aluminum, cerium, neodymium and mischmetal; the addition of which may be
within the range of 8 to 20 weight percent based on the weight of the
total composition. The alloy anode, being easy to manufacture and having
irregular sectional profiles, is free from severe passivation during
electrolytic production using high current density due to its combined
properties. The alloy anode, being highly resistant to corrosion by the
electrolysis solution, requires no activation treatment during the
electrolytic process. The purposefully-designed shapes of the anode permit
good attachment of the deposited product layer and prevent the deposition
from cracking and peeling-off.
Inventors:
|
Fang; Pingwei (Shanghai, CN);
Hu; Wuyu (Shanghai, CN)
|
Assignee:
|
Shanghai Iron & Steel Research Institute (Shanghai, CN)
|
Appl. No.:
|
749532 |
Filed:
|
November 15, 1996 |
Foreign Application Priority Data
| Jun 04, 1991[CN] | 91107417-1 |
Current U.S. Class: |
204/293; 420/418; 420/420; 420/421; 420/900; 429/59; 429/101 |
Intern'l Class: |
C25B 011/04 |
Field of Search: |
204/293
420/900,418,420,421
429/59,101
|
References Cited
U.S. Patent Documents
3436323 | Apr., 1969 | Shimizu et al. | 204/96.
|
4140617 | Feb., 1979 | Dzhaparidze et al. | 204/290.
|
4606804 | Aug., 1986 | Schulke et al. | 204/286.
|
Foreign Patent Documents |
4541201 | Nov., 1970 | JP.
| |
462322 | Jan., 1971 | JP.
| |
Other References
Soviet Invention Certificate No. 484893 with English translation.
|
Primary Examiner: Bell; Bruce F.
Attorney, Agent or Firm: Birch Stewart Kolasch & Birch, LLP
Parent Case Text
This application is a continuation-in-part of application Ser. No.
08/449,759 filed on May 25, 1995, now abandoned, which is a continuation
of application Ser. No. 08/170,852 filed on Dec. 21, 1993, now abandoned,
which is a continuation-in-part of application Ser. No. 07/803,221 filed
on Dec. 6, 1991, now abandoned, the entire contents of which are hereby
incorporated by reference.
Claims
We claim:
1. A titanium alloy anode for electrolyzing manganese dioxide, comprising
titanium with additions of at least three other metals selected from the
group consisting of manganese, chromium, silicon, aluminum, cerium,
neodymium and mischmetal, wherein the amount of the addition of at least
three other metals is 8 to 20 percent based on the weight of the total
composition, the amount of chromium if added is more than or equal to 8
percent based on the weight of the total composition, and the amount of
manganese if added is less than 10.5 percent based on the weight of the
total composition.
2. The titanium alloy anode according to claim 1, wherein the alloy
contains 6-8% by weight manganese, 3-5% by weight chromium, 0.006% by
weight cerium, and the balance titanium.
3. The titanium alloy anode according to claim 1, wherein the alloy
contains 10-14% by weight chromium, 0.1-0.2% by weight cerium, 1-3% by
weight neodymium, and the balance titanium.
4. The titanium alloy anode according to claim 1, wherein the alloy
contains 9-10% by weight manganese, 5-6% by weight chromium, 1-3% by
weight aluminum, 0.01% by weight neodymium, and the balance titanium.
5. The titanium alloy anode according to claim 4, wherein the alloy
contains 9.5% by weight manganese, by weight chromium, 3% by weight
aluminum, 0.01% by weight neodymium and the balance titanium.
6. An anode for the electrolytic production of manganese dioxide, said
anode comprising titanium with additions of at least three other metals
selected from the group consisting of manganese, chromium, iron, aluminum,
silicon, cerium, neodymium and mischmetal, the addition of said at least
three other metals being within the range of 8 to 20 percent by weight;
the addition of manganese if added being within the range of 3 to 10
percent by weight; the addition of chromium if added being within the
range of 3 to 17 percent by weight; the addition of iron if added being
within the range of 0.5 to 5 percent by weight; the addition of aluminum
if added being within the range of 1 to 3 percent by weight; the addition
of silicon if added being within the range of 0.1 to 0.2 percent by
weight; the addition of cerium if added being about 0.006 percent by
weight; the addition of neodymium if added being about 0.01 percent by
weight, and the addition of mischmetal if added being about 1.0 percent by
weight, all of said percents based on the total composition by weight.
7. The titanium alloy anode according to claim 6, wherein the alloy
contains iron in the range of from zero to less than 5 weight percent
based on the total composition by weight.
8. The titanium alloy anode according to claim 6, wherein the alloy
contains 1-2% by weight iron, about 14 or 15% by weight chromium, and 1-3%
by weight aluminum, and the balance titanium.
9. The titanium alloy anode according to claim 6, wherein the alloy
contains about 1-2% by weight iron, about 18% by weight manganese,
0.1-0.2% by weight silicon, and the balance titanium.
10. The titanium alloy anode according to claim 6, wherein the alloy
contains 2-5% by weight iron, 4-6% by weight manganese, 3-5% by weight
chromium, a minor amount of neodymium, and the balance titanium.
11. The titanium alloy anode according to claim 6, wherein the alloy
contains 0.5-3% by weight iron, 3-5% by weight manganese, 6-8% by weight
chromium, a minor amount of mischmetal, and the balance titanium.
Description
BACKGROUND OF INVENTION
The present invention relates to an anode for V/ electrolysis, and more
particularly, to a titanium alloy anode for electrolyzing manganese
dioxide. Electrolytic manganese dioxide, which is an indispensable active
material for use as a positive pole in producing a dry battery of
manganese-zinc series, takes part directly in the discharge reaction. The
quality and the price of the dry battery depend greatly on the product
quality of manganese dioxide.
Lead, graphite and pure titanium anodes are most commonly employed in
producing electrolytic manganese dioxide. So far as anode materials
themselves are concerned, the lead and graphite anodes easily contaminate
the manganese dioxide product, so that the product quality is decreased.
Moreover, these anodes have short service life, and the frequent change of
the anodes requires much time and labor.
The pure titanium anode has the following disadvantages: (1) It is
passivated easily so as to often cause fluctuations in cell voltage,
resulting in an increased consumption of electricity, poor control of
product quality and limited permissible current density; (2) During each
of the electrolytic cycles, the anode also needs an activation treatment
which increases the production costs and makes the process complicated to
carry out; (3) This anode is not sufficient to resist the corrosion by the
electrolysis solutions and its useful life is short.
One of the technical solutions to overcome the disadvantages of pure
titanium anode was suggested in U.S. Pat. No. 4,140,617, which described
an anode with noble-metal coatings. These coatings could only be applied
under high temperature conditions which made it difficult for the coatings
to bond to the surface of pure titanium base metal. This approach was
apparently not economical to practice and unreliable to use.
The Soviet Invention Certificate No. 484893 suggested an anode material for
producing electrolytic manganese dioxide, in which the alloying element of
manganese in 6-16 weight percent was added to the titanium metal to
improve its resistance to passivation. This approach was effective in
overcoming the problem of passivation, but the problems of brittleness and
difficulty in controlling the manganese alloying element had arisen.
These problems had prevented the alloy from being widely used by the
electrolysis industry.
So far as the shapes of the anode materials themselves are concerned, sound
attachment of the deposited manganese dioxide product could not be
obtained on the conventional bar or plate anodes commonly used, and the
deposition-induced stresses often caused cracking and peeling-off of the
product, resulting in a product with poor quality. U.S. Pat. No. 3,436,323
suggested a method for making the surface of the anode in an aventurine
form by sandblasting, which proved to have limited efficacy in overcoming
the above-mentioned problems.
OBJECTS OF INVENTION
The object of the present invention is to provide a titanium alloy anode,
in which multi-element additions are used to improve both the
electrochemical and mechanical properties of the said alloy. It is another
object of the invention to provide a titanium alloy anode in the form of
non-conventional type in order to ensure good attachment of deposition to
the anode surface and to prevent the deposition from cracking and peeling
off.
SUMMARY OF INVENTION
The anode of the present invention is made of titanium with additions of at
least three other different metals selected from the group consisting of
manganese, chromium, iron, silicon, aluminum, cerium, neodymium and
mischmetal; the addition of which may be within the range of 8 to 20
weight percent based on the weight of the total composition.
In a preferred composition of the titanium alloy anode according to the
invention the amount of chromium is more than or equal to 8 percent by
weight based on the total weight of the alloy anode composition and the
amount of manganese is less than 10.5 weight percent based on the weight
of the total composition.
In a particularly preferred composition of titanium alloy anode according
to the invention the amount of iron may be greater than or equal to zero
and less than 5 weight percent, and the amount of manganese is greater
than or equal to zero and less than 10.5 percent be weight, all based on
the weight of the total composition.
A cross-section of the titanium alloy anode of the present invention takes
a non-conventional shape, and it is preferable to make the surface of the
anode in a near-corrugated form or the surface thereon with some regular
projections, wherein the opposite surfaces of the anode may be formed into
concave or convex patterns or recesses, in order to ensure sound
attachment of the deposition, and to prevent any cracking or peeling-off
of the deposition, and thus making the activation treatment unnecessary.
The said anode is highly resistant to corrosion by electrolysis solutions.
In addition, a good attachment of deposited product can be obtained by
using the specially designed anode having non-conventional sections, and
any cracking or peeling-off of the deposit during electrolysis by
electrodeposition stress can also be prevented, as well as ensuring the
quality of the product.
BRIEF DESCRIPTION OF DRAWINGS
The present invention will be more fully understood by the following
examples in conjunction with the accompanying drawings, wherein: FIGS. 1
to 4 are cut away views of four kinds of the titanium alloy anodes in
accordance with the invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
Example 1
An electrode for self-consumable remelting is made by pressing crushed
sponge titanium with an evenly distributed metallic mixture comprising 6-7
wt % chromium, 15-16 wt % manganese, 2-3 wt % iron and a minor amount of
cerium. The electrode is then remelted under vacuum, and cast into an
ingot. However, partial pressure or inert gas can be used if required. The
said ingot is forged and hot rolled, and then shaped into an anode taking
one of the forms shown in FIGS. 1 to 4. The said titanium alloy anode has
a thickness of 1.5-6 mm and a width of 30-120 mm. The length of said anode
is determined according to the depth of the electrolysis bath
(electrolyzer). Table 1 shows the typical mechanical properties of thus
obtained titanium alloy material, in which the examples are taken from the
rods (.PHI.19 mm) and are heat treated at 800.degree. C. for 1 hour and
water quenched.
TABLE 1
______________________________________
Typical Mechanical Properties of the Invented Anode Material
0.2 .delta..sub.b
.delta..sub.5
.psi. .sup..alpha. *
Bending Angle
(MPa) (MPa) (%) (%) (N .multidot. m)
(d = 7.5 mm)
______________________________________
1097 1097 17 54 20 50.degree.
______________________________________
The said anode exhibits an electrical resistance of 105 .mu..OMEGA.cm and
the thermal conductivity (.lambda.) is shown in Table 2 and the Young's
Modulus of the alloy is shown in Table 3.
TABLE 2
______________________________________
Thermal Conductivity of the
Invented Alloy (.lambda.) (cal./cm.sec.Deg)
temp. (.degree.C.)
25 100 200 300 400 500 600 700
______________________________________
.lambda.
0.014 0.018 0.024
0.028 0.034
0.037 0.044
0.051
______________________________________
TABLE 3
______________________________________
Modulus of Elasticity of the Invented Alloy (kg/mm.sup.2)
Temp. (.degree.C.)
Room
Temp. 100 200 300 400
______________________________________
Elasticity
17000 10500 10300 10200 9800
______________________________________
It can be seen that the mechanical properties of the anode material in
accordance with the invention are acceptable for use in the electrolytic
production of manganese dioxide. The said anode is used under the
following conditions and the results of the application are shown in Table
4.
Electrolysis conditions:
Electrolyte: MnSO.sub.4 100 g per liter; H.sub.2 SO.sub.4 25 g per liter
Bath temperature: 90.degree.-100.degree. C.
TABLE 4
__________________________________________________________________________
Application Results of the Invented Anode
Current
Area of
Duration of
MnO.sub.2
Initial Bath
Max. Bath
Average
MnO.sub.2 Content
Density
Anode
Electrolysis
Obtained
Voltage
Voltage
Bath Voltage
of product
(A/m.sup.2)
(m.sup.2)
(h) (Kg) (V) (V) (V) (%)
__________________________________________________________________________
115 17.8
411 1438.4
2.1 3.3 2.84 90.19
76 27.5
532 1750 1.95 2.9 2.64 90.72
53 38.8
964 3460 1.9 2.3 2.15 90.95
__________________________________________________________________________
Under the above-mentioned conditions, the deposited product layer attaches
well to the surface of the said anode. The discharge performance of the
battery of manganese dioxide thus obtained meets the requirements, and the
stripped anode is used to resume the electrolysis cycle without the need
for the activation treatment. The corrosion rate of said anode, when
tested in a typical electrolysis solution containing 40 g H.sub.2 SO.sub.4
per liter and 130 g MnSO.sub.4.H.sub.2 O per liter, at a bath temperature
of 60.degree. C., is 0.007 g/m.sup.2.h. The anode of the present
invention, when placed in a commercial electrolyzer with no current
passing for 200 hours, is free from corrosion while the pure titanium
example for comparison is severely corroded under the same conditions.
Example 2
A mixture comprising 14-17 wt % chromium, 1-2 wt % iron and 1-3 wt %
aluminum is evenly added to the sponge titanium. The said mix is pressed
into an electrode for self-consumable remelting. The electrode is remelted
and cast into an ingot under vacuum. The said ingot is forged and hot
rolled and then shaped into an anode taking one of the forms shown from
FIGS. 1 to 4. The said anode is good in terms of mechanical performance
for the electrolytic production of manganese dioxide. The electrolysis is
carried out under the following conditions.
Electrolysis solution: MnSO.sub.4 70-120 g/l and H.sub.2 SO.sub.4 25-50 g/l
Bath temperature: .gtoreq.90.degree. C.
Current density: 8 OA/M.sup.2
Average voltage across the bath: 2.5 V
The duration of the electrolysis: 558 h
It is observed by visual inspection that the said anode is good in
appearance and free from passivation.
Example 3
A mixture comprising 18-20 wt % manganese, 1-2 wt % iron and 0.1-0.2 wt %
silicon is evenly added to the sponge titanium and the said mix is then
pressed into an electrode to be remelted under vacuum, or partial pressure
or inert gas if required, and cast into an ingot. The said ingot is forged
and hot rolled, and then shaped into an anode taking one of the forms
shown in FIGS. 1 to 4. The said anode is good in terms of mechanical
performance for electrolytic production of manganese dioxide. The
electrolysis is carried out under the following conditions:
Electrolytes: MnSo.sub.4 70-120 g/l and H.sub.2 SO.sub.4 25-50 g/l
Bath temperature: .gtoreq.90.degree. C.
Current density: 8 OA/M.sup.2
The duration of the electrolysis: 200 h
Average bath voltage: 2.8 V
It is observed by visual inspection that the said anode is good in
appearance and free from passivation.
Example 4
A mixture comprising 4-6 wt % manganese, 3-5 wt % chromium, 2-5 wt % iron
and a minor amount of neodymium is evenly added to the sponge titanium and
the said mix is pressed into an electrode to be remelted in a vacuum
consumable melting furnace. The electrode is remelted and cast into an
ingot. The said ingot is forged and hot rolled, and then shaped into an
anode taking one of the forms shown in FIGS. 1 to 4. The said anode is
good in terms of mechanical performance for the electrolytic production of
manganese dioxide. The electrolysis is carried out under the following
conditions:
Electrolyte: MnSO.sub.4 70-120 g/l and H.sub.2 SO.sub.4 25-50 g/l
Bath temperature: .gtoreq.90.degree. C.
Current density: 10 OA/M.sup.2
Average bath voltage: 3.3 V
The duration of the electrolysis: 375 h
It is observed by visual inspection that the said anode is good in
appearance and free from passivation.
Example 5
A mixture comprising 6-8 wt % chromium, 0.5-3 wt % iron, 3-5 wt % manganese
and a minor amount of mischmetal is evenly added to the sponge titanium,
and the mix is pressed into an electrode to be remelted under vacuum. The
said electrode is remelted and cast into an ingot. The said ingot is
forged and hot-rolled into an anode, taking one of the forms shown in
FIGS. 1 to 4. The said anode is good in terms of mechanical performance
for the electrolytic production of manganese dioxide. The electrolysis is
carried out under the following conditions:
Electrolyte: 70-120 g/l MnSO.sub.4 and 25-50 g/l H.sub.2 SO.sub.4
Bath temperature: .gtoreq.90.degree. C.
Current density: 200 A/M.sup.2
Average voltage across the bath: 4.3 V
The duration of the electrolysis: 200 h
It is observed by visual inspection that the said anode is good in
appearance and free from passivation.
Example 6
An electrode for self-consumable remelting was made by pressing the crushed
sponge titanium with evenly distributed metallic mixture comprising 3-5 wt
% chromium, 6-8 wt % manganese and 0.006% cerium. The electrode was then
remelted under vacuum; however, partial pressure or inert gas can be used
if required, and cast into an ingot. The said ingot was forged and hot
rolled, and then it was shaped into an anode taking one of the forms shown
in FIGS. 1 to 4. The said titanium alloy anode has a thickness of 1.5-6 mm
and a width of 30-120 mm. The length of the said anode was determined
according to the depth of electrolysis bath (electrolyzer). Table 5 shows
the typical mechanical properties of thus obtained titanium alloy
material, in which the examples are taken from the rods (.PHI. 19 mm) and
are heat treated at 800.degree. C. for 1 hour and water quenched.
TABLE 5
______________________________________
Typical Mechanical Properties of the Invented Anode Material
.delta..sub.0.2
.delta..sub.b
.delta..sub.5
.psi. .sup..alpha. *
Bending Angle
(MPa) (MPa) (%) (%) (N .multidot. m)
(d = 7.5 mm)
______________________________________
1000 1000 18 55 20 80.degree.
______________________________________
The said anode exhibits an electrical resistance of 10 A.mu..OMEGA.-cm and
a thermal conductivity (.lambda.) is shown in Table 6 and Young's Modulus
(E) of the alloy is shown in Table 7.
TABLE 6
______________________________________
Thermal conductivity of
the Invented Alloy (.lambda.) (cal./cm.sec.Deg)
temp. (.degree.C.)
25 100 200 300 400 500 600
______________________________________
A 0.014 0.018 0.024 0.028 0.034 0.037 0.044
______________________________________
TABLE 7
______________________________________
Modulus of Elasticity of the Invented Alloy (kg/mm.sup.2)
Temp. (.degree.C.)
Room Temp.
100 200 300
______________________________________
Elasticity
10700 10500 10300 10200
______________________________________
It can be seen that mechanical properties of the anode material in
accordance with the invention are acceptable for use in the electrolytic
production of manganese dioxide. The said anode was used under the
following conditions and the results are shown in Table 8.
Electrolysis conditions:
Electrolyte: MnSO.sub.4 100 g per liter; H.sub.2 SO.sub.4 25 g per liter
Bath temperature: 90.degree.-100.degree. C.
TABLE 8
__________________________________________________________________________
Results of the Invented Anode
Current
Area of
Duration of
MnO.sub.2
Initial Bath
Max. Bath
Average
MnO.sub.2 Content
Density
Anode
Electrolysis
Obtained
Voltage
Voltage
Bath Voltage
of product
(A/m.sup.2)
(m.sup.2)
(h) (Kg) (V) (V) (V) (%)
__________________________________________________________________________
120 17.8
411 1450 2.2 3.5 3 90.19
80 27.5
532 1800 2.05 3.0 2.8 90.72
60 38.8
964 3510 2 2.5 2.2 90.95
__________________________________________________________________________
Under the above-mentioned condition, the deposited product layer attached
well to the surface of the said anode without any obvious peeling. The
discharge performance of the battery of manganese dioxide thus obtained
satisfied the requirements and the stripped anode was used to resume the
electrolysis cycle without the need for activation treatment. The
corrosion rate of the said anode, when tested in a typical electrolysis
solution containing 40 g/l H.sub.2 SO.sub.4 per liter and 130 g/l
MnSO.sub.4 --H.sub.2 O per liter, at a bath temperature of 60.degree. C.,
was found to be 0.068 g/m.sub.2.h. The anode of the present invention,
when placed in a commercial electrolyzer with no current passing for 200
hours, was free from corrosion, while the pure titanium example for
comparison was severely corroded under the same conditions.
Example 7
A mixture comprising 10-14 wt % chromium, 0.1-0.2 wt % silicon and 1-3 wt %
aluminum was evenly added to the sponge titanium. The said mix was pressed
into an electrode for self-consumable remelting. The electrode was
remelted and cast into an ingot under vacuum. The said ingot was forged
and hot rolled and then it was shaped into an anode taking one of the
forms shown in FIGS. 1 to 4. The said anode was good in terms of
mechanical performance for electrolytic production of manganese dioxide.
The electrolysis was carried out under the following conditions.
Electrolysis solution: MnSO.sub.4 70-120 g/l and H.sub.2 SO.sub.4 25-60 g/l
Bath temperature: .gtoreq.90.degree. C.
Current density: 8 OA/m.sup.2
Average voltage across the bath: 2.5 V
The duration of the electrolysis: 558 h
It was observed by visual inspection that the said anode was good in
appearance and free from passivation.
Example 8
A mixture comprising 9-10 wt % manganese, 5-6wt % chromium, 1-3 wt %
aluminum and 0.01 wt % neodymium or its mischmetal was evenly added to the
sponge titanium and the said mix was then pressed into an electrode to be
remelted under vacuum; however, partial pressure or inert gas can be used
if required, and cast into an ingot. The said ingot was forged and hot
rolled, and then it was shaped into an anode taking one of the forms shown
in FIGS. 1 to 4. The said anode was good in terms of mechanical
performance for electrolytic production of manganese dioxide. The
electrolytic was carried out under the following conditions:
Electrolyte: MnSO.sub.4 70-120 g/l and H.sub.2 SO.sub.4 25-50 g/l
Bath temperature: .gtoreq.90.degree. C.
Current Density: 100 A/m.sup.2
The duration of the electrolysis: 375 h
Average bath voltage: 3.3 V
It was observed by visual inspection that the said anode was good in
appearance and free from passivation.
As an illustration of an alloy anode useful according to Example 8 of the
invention, the alloy contains 5 percent by weight chromium, 9.5 percent by
weight manganese, 3 percent by weight aluminum, 0.01 percent by weight
neodymium, and the balance titanium.
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